MY149160A - Method of converting c9 aromatics-comprising mixtures to xylene isomers - Google Patents
Method of converting c9 aromatics-comprising mixtures to xylene isomersInfo
- Publication number
- MY149160A MY149160A MYPI20045042A MYPI20045042A MY149160A MY 149160 A MY149160 A MY 149160A MY PI20045042 A MYPI20045042 A MY PI20045042A MY PI20045042 A MYPI20045042 A MY PI20045042A MY 149160 A MY149160 A MY 149160A
- Authority
- MY
- Malaysia
- Prior art keywords
- xylene isomers
- aromatics
- feed
- converting
- product stream
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/08—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
- C07C6/12—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
- C07C6/126—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring of more than one hydrocarbon
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/08—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
- C07C6/12—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/08—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
[0114] DISCLOSED HEREIN IS A METHOD OF MAKING XYLENE ISOMERS. MORE SPECIFICALLY, THE METHOD INCLUDES CONTACTING A C? AROMATICS-COMPRISING FEED WITH A CATALYST UNDER CONDITIONS SUITABLE FOR CONVERTING THE FEED TO AN INTERMEDIATE PRODUCT STREAM COMPRISING XYLENE ISOMERS, SEPARATING AT LEAST A PORTION OF THE XYLENE ISOMERS FROM THE INTERMEDIATE PRODUCT STREAM, AND RECYCLING TO THE FEED THE XYLENE ISOMERS-LEAN INTERMEDIATE PRODUCT STREAM. ALTERNATIVELY, THE METHOD OF MAKING XYLENE ISOMERS INCLUDES CONTACTING A FEED COMPRISING C? AROMATICS AND LESS THAN ABOUT 30 WT.% BENZENE, BASED ON THE TOTAL WEIGHT OF THE FEED, WITH A NON-SULFIDED, LARGE-PORE ZEOLITE IMPREGNATED WITH A GROUP VIB METAL OXIDE, UNDER CONDITIONS SUITABLE FOR CONVERTING THE FEED TO A PRODUCT STREAM COMPRISING XYLENE ISOMERS. THE DISCLOSED METHOD IS CHARACTERIZED BY UNEXPECTEDLY HIGH RATIOS OF XYLENE ISOMERS TO ETHYLBENZENE, XYLENE ISOMERS TO C? AROMATICS (E.G., METHYLETHYLBENZENE), XYLENE ISOMERS TO C?? AROMATICS, TRIMETHYLBENZENE TO METHYLETHYLBENZENE, BENZENE TO ETHYLBENZENE, IN THE PRODUCT OF THE CONVERSION, AND THE HIGH CONVERSION OF C? AROMATICS AND METHYLETHYLBENZENE.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/794,932 US20050197518A1 (en) | 2004-03-04 | 2004-03-04 | Method of converting C9 aromatics-comprising mixtures to xylene isomers |
Publications (1)
Publication Number | Publication Date |
---|---|
MY149160A true MY149160A (en) | 2013-07-31 |
Family
ID=34912383
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MYPI20045042A MY149160A (en) | 2004-03-04 | 2004-12-06 | Method of converting c9 aromatics-comprising mixtures to xylene isomers |
Country Status (12)
Country | Link |
---|---|
US (1) | US20050197518A1 (en) |
EP (1) | EP1720816A1 (en) |
JP (1) | JP4832422B2 (en) |
KR (2) | KR20120081225A (en) |
CN (1) | CN1918089B (en) |
AU (1) | AU2004318012A1 (en) |
BR (1) | BRPI0418580A (en) |
CA (1) | CA2553514C (en) |
MY (1) | MY149160A (en) |
RU (1) | RU2354640C2 (en) |
TW (1) | TWI377188B (en) |
WO (1) | WO2005095309A1 (en) |
Families Citing this family (25)
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US7507273B1 (en) * | 2005-06-20 | 2009-03-24 | 6Solutions, Llc | Chromatographic rectification of ethanol |
US20070049780A1 (en) * | 2005-08-30 | 2007-03-01 | Schwartz Hilary E | Methods of making xylene isomers |
US7553998B2 (en) * | 2006-06-21 | 2009-06-30 | Uop Llc | Energy-efficient process for para-xylene production |
US7692052B2 (en) * | 2006-12-29 | 2010-04-06 | Uop Llc | Multi-zone process for the production of xylene compounds |
JP5462789B2 (en) * | 2007-07-06 | 2014-04-02 | ユーオーピー エルエルシー | Multi-zone process for the production of diesel fuel and aromatic compounds |
US20100029467A1 (en) * | 2008-07-30 | 2010-02-04 | Tomoyuki Inui | Multiple zeolite catalyst |
US8653315B2 (en) | 2008-07-30 | 2014-02-18 | King Fahd University Of Petroleum And Minerals | Multiple zeolite catalyst and method of using the same for toluene disproportionation |
CN102295284B (en) * | 2010-06-28 | 2013-05-15 | 通用电气公司 | Method for converting carbon into oxides of carbon as well as method and device for hydrocarbon cracking |
US8557028B2 (en) | 2011-03-31 | 2013-10-15 | Uop Llc | Binderless zeolitic adsorbents, methods for producing binderless zeolitic adsorbents, and adsorptive separation processes using the binderless zeolitic adsorbents |
US9309170B2 (en) * | 2011-11-14 | 2016-04-12 | Uop Llc | Aromatics isomerization using a dual-catalyst system |
US8697928B2 (en) * | 2011-12-15 | 2014-04-15 | Uop Llc | Process and apparatus for para-xylene production using multiple adsorptive separation units |
KR101359974B1 (en) * | 2011-12-27 | 2014-02-12 | 주식회사 포스코 | Non-Platinum Transaklylation Catalyst for Mixed Xylene Production from Aromatic Compounds |
CN104334515A (en) | 2012-04-19 | 2015-02-04 | 沙特阿拉伯石油公司 | Combined heavy reformate dealkylation-transalkylation process for maximizing xylenes production |
US20140100402A1 (en) * | 2012-10-09 | 2014-04-10 | Exxonmobil Chemical Patents Inc. | Recovery of Olefins from Para-Xylene Process |
PT3105201T (en) * | 2014-02-13 | 2019-12-24 | Bp Corp North America Inc | Energy efficient fractionation process for separating the reactor effluent from tol/a9+ translakylation processes |
JP6254882B2 (en) | 2014-03-26 | 2017-12-27 | コスモ石油株式会社 | Method for producing xylene |
US10173950B2 (en) | 2017-01-04 | 2019-01-08 | Saudi Arabian Oil Company | Integrated process for the production of benzene and xylenes from heavy aromatics |
US10035742B1 (en) | 2017-05-26 | 2018-07-31 | Saudi Arabian Oil Company | Process for maximizing xylenes production from heavy aromatics for use therein |
US10464868B2 (en) | 2017-05-26 | 2019-11-05 | Saudi Arabian Oil Company | Process for maximizing production of xylenes from heavy reformate without purge |
US10252958B2 (en) | 2017-05-26 | 2019-04-09 | Saudi Arabian Oil Company | Process for xylene production with energy optimization |
US10696609B2 (en) | 2018-10-15 | 2020-06-30 | Saudi Arabian Oil Company | Integrated process for maximizing production of para-xylene from full reformate |
US10894755B2 (en) | 2018-10-15 | 2021-01-19 | Saudi Arabian Oil Company | Integrated process for optimum production of para-xylene |
US10501389B1 (en) | 2018-10-25 | 2019-12-10 | Saudi Arabian Oil Company | Process and system for the production of para-xylene and benzene from streams rich in C6 to C12+ aromatics |
CN112745932B (en) | 2019-10-30 | 2022-07-15 | 中国石油化工股份有限公司 | Method for producing light aromatic hydrocarbon |
US11103859B2 (en) * | 2020-01-06 | 2021-08-31 | Uop Llc | UZM-54 and transalkylation process using same |
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US3476821A (en) * | 1968-02-29 | 1969-11-04 | Texaco Inc | Disproportionation of alkyl aromatics with decationized mordenite containing a sulfided metal |
US3562345A (en) * | 1968-09-18 | 1971-02-09 | Universal Oil Prod Co | Crystalline aluminosilicate-alumina composition and transalkylation therewith |
US3677973A (en) * | 1970-03-16 | 1972-07-18 | Universal Oil Prod Co | Transalkylation of alklaromatic hydrocarbons in contact with a zeolite catalyst composition |
US4041091A (en) * | 1976-02-19 | 1977-08-09 | Uop Inc. | Fractionation of aromatic streams |
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JPS5439024A (en) * | 1977-09-01 | 1979-03-24 | Nosonobuichi Masuriyans Gudaru | Process for preparing benzene and xylene |
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JPS58204817A (en) * | 1982-05-19 | 1983-11-29 | Teijin Yuka Kk | Production of crystalline aluminosilicate zeolite |
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-
2004
- 2004-03-04 US US10/794,932 patent/US20050197518A1/en not_active Abandoned
- 2004-11-16 JP JP2007501767A patent/JP4832422B2/en not_active Expired - Fee Related
- 2004-11-16 KR KR1020127014196A patent/KR20120081225A/en not_active Application Discontinuation
- 2004-11-16 CA CA2553514A patent/CA2553514C/en not_active Expired - Fee Related
- 2004-11-16 CN CN2004800416971A patent/CN1918089B/en not_active Expired - Fee Related
- 2004-11-16 RU RU2006131587/04A patent/RU2354640C2/en not_active IP Right Cessation
- 2004-11-16 AU AU2004318012A patent/AU2004318012A1/en not_active Abandoned
- 2004-11-16 WO PCT/US2004/038075 patent/WO2005095309A1/en active Application Filing
- 2004-11-16 KR KR1020067018002A patent/KR101189439B1/en not_active IP Right Cessation
- 2004-11-16 BR BRPI0418580-3A patent/BRPI0418580A/en not_active Application Discontinuation
- 2004-11-16 EP EP04821876A patent/EP1720816A1/en not_active Withdrawn
- 2004-12-06 MY MYPI20045042A patent/MY149160A/en unknown
- 2004-12-16 TW TW093139197A patent/TWI377188B/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
BRPI0418580A (en) | 2007-06-19 |
KR20120081225A (en) | 2012-07-18 |
TW200530148A (en) | 2005-09-16 |
KR20060135803A (en) | 2006-12-29 |
AU2004318012A1 (en) | 2005-10-13 |
JP2007526301A (en) | 2007-09-13 |
US20050197518A1 (en) | 2005-09-08 |
WO2005095309A1 (en) | 2005-10-13 |
EP1720816A1 (en) | 2006-11-15 |
CA2553514C (en) | 2012-01-10 |
KR101189439B1 (en) | 2012-10-12 |
RU2354640C2 (en) | 2009-05-10 |
TWI377188B (en) | 2012-11-21 |
CN1918089A (en) | 2007-02-21 |
JP4832422B2 (en) | 2011-12-07 |
RU2006131587A (en) | 2008-04-10 |
CN1918089B (en) | 2011-06-15 |
CA2553514A1 (en) | 2005-10-13 |
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